US2955124A - Manufacture of organolead compounds - Google Patents

Description

Unite States Patent MANUFA'CTURE'OF ORGAN OL EAD CONIPOUNDS Sidney Blitzer and Tillmon H. Pearson, Baton Rouge, La., assignor'sto Ethyl Corporation, New York, N.Y., a corp'oration of Delaware No Drawing. Filed Feb; '27, 1957, Ser. No. 642,636

6 Claims. (Cl. 260 -437) This invention relates' toa process for the manufacture of organ'olead compounds. More specifically, it is particularly directed to' a new and novel process for the manufacture of tetraalk-yllead compounds, especially the important antiknock' material, tetraethyllead.

The processes heretofore employed on a substantial scale are best illustrated by reference to the production of tetraethyllead. This material is in wide usage as an an'tiknock' agent in the operation of internal combustion engines. The commercial process has generally been highly successful, but has certain inherent disadvantages not heretofore circumvented. The process proceeds by reacting a sodium-lead alloy, of composition controlled to correspond substantially to-NaPb, with ethyl chloride according to the following equation:

With the highest yields obtained thereby, only some 20'percent of the lead present in the NaPb-alloy is converted to tetraethyllead. This conversion of lead to tetraethyllead has not been materially changed in many years, apparently because of an inherent limitation corresponding to the above equation. In this reaction, then, at least 75 percentof the lead originally employed is not alkylated. Large quantities of lead must then be recovered and reprocessed to NaPb alloy in order tomake it economical. A further disadvantage of such a large quantity of unreacted leadis that Valuable reaction space in the reactor is occupied by materials which are essentially inert for the manufacture of tetraethyllead under present conditions and mode of operation.

Other reaction processes for the production of hydrocarbon-lead ompounds, especially tetraethyllead, have been devised to eensuine the lead produced in the above equation. While such processes are satisfactory from the standpoint of lead consumption, they suffer an additional drawback in common with the prment commercial process in that they require organo halide as the ethylating agent. jOne such'proce'ss is? thatdescribed' in U.S. Patent-2,535,190 wherein lead; as' for example that pro duced in the commercial process, is treated with metallic magnesium and ethyl chloride in the presence of a-cata- 'lyst, preferably; an alkylether. Thus, inthis process as well as theabov'e mentioned alloy process, the tetraethyllead manufacturing operatioiris restricted by the necessary balance-betweenthesinefallic so dium required and the organic chlorine in the ethyl chloride. A classical method for the nianufaeture of tetraethyllead which likewise requires; strict balance 'between metallic magiiesiiifn an organic halide is reaction of these-called Gi-igriard reagent, for instance ethyl magnesium chloride, 7

with lead chloride. &

More recently, a process has been developed which overcomes the disadvantages of the above and other prior art processes,v produces ahigher yield of the orproduct, and greater consumption of the lead metal. A 'typicalexaifiple of new developmentis the reaction 0ft). lead organo acid salt with an active organometallic compound, for example, the reaction of lead acetate With'triethyl aluminum. This process is generally satisfactory and a definite improvement over the prior art'processes. However, a need in thisprocess and the aforementioned prior art processes has been to further increase the yield of organolead product, in particular the commercial product tetraethyllead, to an even higher level in order to provide a more economical process. As a result of our work in this field such a process has been found. Y

It is an object of this invention to provide, a novel process for the manufacture of organolead compounds which overcomes the prior art difiiculties and provides such compounds in higher yields. Another objectis, to provide a moreeconomical process for the manufacture of the organolead compounds. A still further object is to provide a new andimproved process for the pro: duction of tetraethyllead in higher yields than obtained heretofore.

It has now beenfoundthat theorganolead compounds can be produced in higher yields than heretofore obtain;- able by reacting a lead organo acid. salt with an active organometallic compound in the presence of an ether. The employment of the ethers as a diluent in such a process results in a substantial increase in yield of the organolead product over that obtained when conducting this particular reaction in the presence of other diluents' as for example the hydrocarbons. An additional benefit is that shorter reaction periods are required for completion of the reaction than required by the prior art processes. In general these benefits are obtained when conducting the reaction of the-lead organic acid salt with active organometallic compounds in the presence of any of' the ethers. However, the polyethers, especially of ethylene glycol and polyethylene glycol, have been found most suitable and in this connection the diinethyl etherof diethylene glycol and dimethoxyethane are particularly satisfactory. In one particularly preferred'en bodiment, the commercial product tetraethyllead is obtained by reacting lead acetate with triethyl the presence of such ethylene glycol ethers.

As stated previously, in general any other be ployed in the process of this invention since it has been found that all ethers produce abeneficial effect onthe reaction. Some criteria of choice of theether to be employed are that they be essentially inert to the reactants, liquid under the reaction conditions and preferably at room temperature, or soluble'in the reaction Generally speaking, the ethers can be non-aromatic,

aromatic, and polyethers. The non-aromatic ethers inether; and the like. When the aromaticether is an 'alky ,aryl ether, we employ, for example, methylphenyl ether; .met-liylo,m, or p tolyl ether; methyl-ot-naphthyl ether;

ethylphenyl ether; ethyl-.o,m, orp-tolyl ether; ethyl-un'aphthylaether; phenyl-n-propyl ether; jisopropylphenyl vether;-n -butylphenyl ether; .n-butyl o tolyl ether; isoatnyln-naphthyl ether; and .thelike. The alkaryl :alkyl ethers which ..we employ can be, for example, benzylmethyl ether; benzylethyl ether; benzyl-n-butyl other; and ,the

like. Examples of the polyethers which are employed are Patented 0a, 4, 1 ea s but under suflicie t pressure to, maintain thereaction mixture liquid, at high yield of tetraethyllead is obtained.

Example VIII When lead benzoate, lead butyrate, or lead oleate are reacted with triethyl aluminum in furan, vinyl butyl ether, anisole, diethyl acetal or dimethyl ether of tetraethy-lene glycol, high yields of tetraethyllead are obtained.

The foregoing examples illustrate typical ethers which are. employed in the process of this invention. In place of the particular ethers employed therein similar results are obtained when the ethers mentioned hereinbefore are substituted, for example di-n-butyl ether, n-amyl methyl ether, diphenyl ether, methylphenyl ether, diethyl'ether of ethylene glycol, dioxane, the diethyl ether of diethylene glycol and the like.

The employment of the ethers as solvents in the present process consistently results in obtaining higher yields of the organolead compound. As a typical illustration of these benefits of the present invention a controlled comparison was made in which lead acetate was reacted with triethyl aluminum under identical conditions employing, in one instance, toluene and in the other instance the dimethyl ether of diethylene glycol as the solvent. It was found that the ether solvent, for the same reaction time and temperature, resulted in a 10 percent increase in yield. Similar and in most instances greater enhancement in yield of the organolead product is obtained when other ether s are compared with other solvents employed heretofore in the reaction of lead organo acid with stable organometallic compounds.

The following examples will demonstrate that embodiment of this invention wherein mixtures of the ether solvent with other solvents are employed.

Example IX Example X The procedure of Example IX was repeated with exssr n ha 3-3 Part at ,.2-dig19 hO i/ ein, d gi tu e wi h 49 part 9? tal ies? we e, m le Th m 3 te rae h ll ad was 90: res t- I Example XI' 1 When Example IX was repeated essentially as described with exception that the solvent comprised 2.8 parts t diethyl ether and 43 parts of toluene with the reaction conducted at the reflux temperature for 1 /2 hours, the yield of tetraethyllead was 91.4 percent.

When this run was duplicated with exception that 8.2

parts of the diethyl ether in the same amount of toluene was employed, the yield of tetraethyllead was 93.7 percent.

When other mixtures of others with the hydrocarbon and other solvents as, for example, organic halides and amines, are employed as described previously, similar results are obtained.

The present invention is concerned with an improvement in the reaction of the lead organo acid salts with the active organometallics. Briefly, this process comprises reacting these compounds at varied temperatures as between about 20 to 200 C. and preferably between 25 and 150 C. However, if desired, thermal stabilizers well known to the art, for example naphthalene and styrene, can be employed to permit the use of higher reaction temperatures without concomitant degradation of the organolead product. Generally the autogenous pressure is employed although the pressure is not critical and the reaction can be conducted at atmospheric or subatmospheric pressure.

The lead organo-acid salt employed in conducting this P oc ss comp se lead pmpou ds w ich the lead is attached to at least 1 carbon-containing radical through an intermediate atomof oxygen or sulphur, that is a chalkogen. Such definition includes also recognized organic acids not having a carboxylic group. Thus the lead salts employed are lead carboxylate, lead thioc'arboxylate, lead phenate'and lead thiophenates. The organic portion can contain other elements'besides carbon and hydrogen, in particular oxygen or other substituents such as halogen which are essentially inert in the reaction. Typical of the lead salts which are employed are lead acetate, lead tetraacetate, lead laurate, lead propionate, lead phenate, lead thiophenate, lead salicylate, lead tallate, lead naphthenate, and the like. Thus in any of the Examples I through XI, these compounds can be substituted for the lead salt employed and similar results are obtained. In preferred embodiments the lead organo acid salt has between 1 and 21 carbon atoms in each acidic radical.

The active organometallic compounds can be any organometallic compound of a metal having a electrode potential of more than 0.3 volt and capable of forming stable organometallic compounds. Included among such metals are the group IA metals such as lithium and sodium, group II metals such as beryllium, magnesium, zinc and calcium, and the group HIT-A metals such as boron, aluminum and the like. The fully organic substituted compounds of the polyvalent metals are preferred, particularly aluminum, but organic compounds of monovalent active metals and partially organo-substituted derivatives of the polyvalent metals are suitable. Further, complex organometallic compounds can be employed, that is, compounds having more than one metal, particularly an alkali or alkaline earth metal and a polyvalent metal therein. Typical examples of the active organometallic compounds which can be employed include ethyl sodium, trimethylalumin-um, methyldiethylaluminum, ethyl lithium, diethylmagnesium, ethyl magnesium chloride, diethylzinc, triet-hylborine, methylethyloctylaluminum, diethylaluminum hydride, sodium aluminum tetraethyl, ethylaluminum sesquichloride, diinethyllindium hydr-ide, tricyclohexylaluminum, phenyl sodium, diphenyl zinc, naphthylsodium, tripropylaluminum, cy clohexyldiethylaluminum, tritolylaliiminum, and the like organometallic compounds including such compounds which are substituted by organic subs'tituents which are essentially inert in the reaction. Ingeneral, however, the alkyl metal compounds, particularly those in which the alkyl groups contain between 1 and 8 carbon atoms, are especially preferred because of their greater availability and ease of formation.

In this process it is also to ,be recognized that the lead organo acid salts are also efiective in conjunction with other inorganic salts, for example, the lead sulphides and oxides The double salts are particularly suitable, for example, the double salt of lead acetate and lead oxide.

The following examples will demonstrate other particular embodiments of this invention employing the aforementioned representative organometallic compounds and lead salts of organo acids.

Example XII To a reaction vessel similar to that employed in Example I was added 52 parts of dimethoxyethane and 8.3 parts of lead acetate. This mixture was heated to 60 C. and then a solution of about 2 parts of diethylm-agnesium in 35 parts diethyl ether was slowly added. The diethyl ether was condensed and removed as it vaporized from the reaction mixture. After a total reaction time of two hours at a temperature up to about 90 C., the mixture was cooled to room temperature and processed as in the preceding examples. The yield of tetraethyllead was 76 percent.

i the presence of dioxane.

Example XIII The procedure of Example I is repeated with exception that 155 531 8 of lead tetraactate are reacted with 4.0 parts of triethylaluminuin in 45mm of the diethyl'ether of diethylene glycol, A high yield of tetraethyllead is obtained. y r Example XIV Tetrabutyllead is obtained in h gh yield when stoichiometric quantities of sodium aluminum tributyl hydride are reacted withle' id Palmitate at60 C. forb hours in Example XV I Employing the procedure of ExampleI, an essentially quantitative yield of tetraethyllead is obtained when lead tetraacetate reacted with sodium aluminum tetraethyl in tetrahydrofuran at the reflux temperature for 1 hour. I

' Example XVI When triphenyl aluminum is reacted with lead stearate in the dimethyl ether of diethylene glycol, tetraphenyl lead is obtained in high yield.

Example XVII An enhanced yield of tetraethyllead is obtained When diethyl zinc is reacted with lead phenolate in the presence of diethyleneglycol diethyl ether at the reflux temperature. e

Example XVIII metallic compounds employed therein. Likewise lead naphthenate, lead citrate, lead salicylate, lead phenol sulfonate, and the like lead organo acid salts can be substituted for the lead compounds employed therein.

From the foregoing description and examples it will be evident that the process is capable of a large number of embodiments without departing from the spirit and scope thereof, Thus the technique of carrying out the reaction including the temperature and pressure, mode of addition, batch and continuous techniques, and the physical state of the reactants can be varied. Being illustrative, it is not intended that the foregoing description shall in any way limit the scope of the present invention. e e e e Having thus described the process of the present invention, what is claimed is: e I e e '1. In a process for the manufacture of a hydrocarbon lead compound which comprises reacting a lead organo acid salt wherein lead is attached to at least one carbon containing radical through an intermediate atom selected from the group consisting of oxygen and sulfur and an active hydrocarbon metal compound of a metal selected from the group consisting of group I-A, II, and HI-A metals having an electrode potential of more than 0.3 volt and wherein the hydrocarbon groups of said active hydrocarbon metal compound are selected from the group consisting. of alkyl, cycloalkyl, and aryl groups having up to and including 10 carbon atoms, the improvement which comprises conducting said reaction in the presence of an ether which is essentially inert to the reactants, liquid under the reaction conditions, and selected from the group consisting of alkyl and aryl others.

2. The process of claim 1 wherein said ether is a polyether.

3. The process of claim 1 wherein said ether is employed in admixture with a hydrocarbon solvent.

4. The process for manufacturing tetraethyllead which comprises reacting lead acetate with triethylaluminum in the presence of the dimethyl ether of diethylene glycol at a temperature between about 25 to C. and recovering tetraethyllead upon completion of the reaction.

5. The process 'of claim 1 wherein said lead organo acid salt is a lead saltof an alkanoic acid, said hydrocarbon metal compound is a group III-A metal alkyl, said ether 'is an alkyl ether, and said reaction is conducted at a temperature between about 25 to 150 C.

6. The process of claim 5 wherein said lead organo acid salt is lead acetateand said group III-A metal alkyl is triethylaluminum.

References Cited the file of this patent 2,859,231 Blitzer et a1. Nov. 4,

Claims (1)

1. IN A PROCESS FOR THE MANUFACTURE OF A HYDROCARBON LEAD COMPOUND WHICH COMPRISES REACTING A LEAD ORGANO ACID SALT WHEREIN LEAD IS ATTACHED TO AT LEAST ONE CARBON CONTAINING RADICAL THROUGH AN INTERMEDIATE ATOM SELECTED FROM THE GROUP CONSISTING OF OXYGEN AND SULFUR AND AN ACTIVE HYDROCARBON METAL COMPOUND OF A METAL SELECTED FROM THE GROUP CONSISTING OF GROUP I-A, II, AND III-A METALS HAVING AN ELECTRODE POTENTIAL OF MORE THAN 0.3 VOLT AND WHEREIN THE HYDROCARBON GROUPS OF SAID ACTIVE HYDROCARBON METAL COMPOUND ARE SELECTED FROM THE GROUP CONSISTING OF ALKYL, CYCLOALKYL, AND ARYL GROUPS HAVING UP TO AND INCLUDING 10 CARBON ATOMS, THE IMPROVEMENT WHICH COMPRISES CONDUCTING SAID REACTION IN THE PRESENCE OF AN ETHER WHICH IS ESSENTIALLY INERT TO THE REACTANTS, LIQUID UNDER THE REACTION CONDITIONS, AND SELECTED FROM THE GROUP CONSISTING OF ALKYL AND ARYL ETHERS.